NR 110.21(4)(d)2.
2. Liquid depths in aeration tanks may not be less than 3 meters (10 feet). The department may allow liquid depths to exceed 5 meters (16 feet) on a case-by-case basis.
NR 110.21(4)(d)3.
3. Baffling or the placement of aeration equipment shall provide positive control of hydraulic short-circuiting through aeration tanks.
NR 110.21(4)(d)4.
4. Process piping, influent channels and inlet structure shall be arranged to provide operational flexibility.
NR 110.21(4)(d)5.
5. Inlets and outlets for each aeration tank unit shall be equipped with valves, gates, stop plates, weirs or other devices to permit controlling the flow to each tank and to maintain a constant liquid level. The hydraulic properties of the system shall permit the peak instantaneous design flow to be carried with any single aeration tank unit out of service.
NR 110.21(4)(d)6.
6. Channels and pipes carrying liquids with suspended solids shall be designed to maintain self-cleansing velocities or shall be agitated to keep the solids in suspension at all rates of flow within the design limits.
NR 110.21(4)(d)7.
7. All aeration tanks shall have a freeboard of not less than 46 centimeters (18 inches).
NR 110.21(5)(a)(a) General. The aeration system shall be capable of meeting the oxygen requirements of the activated sludge system, or of maintaining adequate mixing of the mixed liquor suspended solids, whichever is greater.
NR 110.21(5)(b)1.1. Aeration equipment shall be capable of maintaining a minimum mixed liquor dissolved oxygen concentration of 2 milligrams per liter.
NR 110.21(5)(b)2.
2. In the absence of experimentally determined values, the design oxygen requirements for all activated sludge processes shall be 1.1 kilograms oxygen per kilogram peak hour BOD
5 (1.1 pounds oxygen per pound peak hour BOD
5) removed in the aeration tanks, with the exception of the extended aeration process, for which the value shall be 1.5 kilograms oxygen per kilogram peak hour BOD
5 (1.5 pounds oxygen per pound peak hour BOD
5) to include endogenous respiration requirements.
NR 110.21(5)(b)3.
3. To provide nitrification, the oxygen requirement for oxidizing ammonia shall be added to the requirement in subd.
2. for carbonaceous BOD
5 removal and endogenous respiration requirements. In the absence of experimentally determined values, the nitrogen oxygen demand (NOD) shall be 4.6 kilograms of oxygen per kilogram removed peak hour total Kjeldahl nitrogen (TKN) (4.6 pounds oxygen per pound removed peak hour TKN).
NR 110.21(5)(c)1.1. The design of the aerator system to provide the oxygen requirements calculated in accordance with par.
(b) shall be done using standard design equations for diffused and mechanical aeration systems. Calculations shall incorporate such factors as tank depth, alpha factor of the waste, beta factor of the waste, certified aerator oxygen transfer efficiency, minimum aeration tank dissolved oxygen concentration, critical wastewater temperature and altitude of the wastewater treatment facility.
NR 110.21(5)(c)2.
2. In the absence of specific design information, the air requirements for diffused aerators shall be calculated using an oxygen transfer efficiency of 7% in clean water under standard test conditions. The air requirements for mechanical aerators shall be based on a transfer rate of 1.2 kilograms oxygen per kilowatt-hour (2 pounds oxygen per horsepower-hour) in clean water under standard test conditions.
NR 110.21(5)(d)
(d) Mixing requirements. The following minimum requirements shall be met to insure adequate mixing of mixed liquor suspended solids.
NR 110.21(5)(d)1.
1. Diffused aeration systems shall be capable of delivering a minimum air flow rate of 20 cubic meters per minute per 1,000 cubic meters (20 cubic feet per minute per 1,000 cubic feet) of aeration volume.
NR 110.21(5)(d)2.
2. Mechanical aerators shall deliver a minimum of 15 kilowatts per 1,000 cubic meters (0.6 horsepower per 1,000 cubic feet) of aeration volume.
NR 110.21(5)(e)
(e) Other air-use demands. The aeration system shall also be capable of providing the air required for channel aeration, air-lift pumps, aerobic digesters, and any other air-use demand.
NR 110.21(6)(a)1.1. Multiple blowers shall be provided. The blowers shall be sized to meet the maximum air demand with the largest blower out of service. The design shall also provide for varying the volume of air delivered in proportion to the air demand of the plant.
NR 110.21(6)(a)2.
2. Diffusers and air piping shall be capable of supplying the peak hour air demand or 200% of the design average air demand, whichever is larger.
NR 110.21(6)(a)3.
3. The arrangement of diffusers shall permit their removal for inspection, maintenance and replacement without dewatering aeration tanks or channels and without shutting off the air supply to other diffusers in the treatment system. The department may waive this requirement for systems with multiple aeration tanks provided the treatment efficiency of the system can be maintained with one aeration tank out of service.
NR 110.21(6)(b)1.1. Multiple mechanical aeration units shall be designed and located so as to meet the peak hour oxygen demand or 200% of the design average oxygen demand, whichever is larger, with one unit out of service.
NR 110.21(6)(b)2.
2. Due to high heat loss, the mechanical aerators shall be protected from freezing.
NR 110.21(6)(c)
(c) Pure oxygen. Where pure oxygen is proposed, supporting data from pilot plant installations or full-scale installations similar to the one proposed shall be submitted to justify the aerator loading rate and the amount and type of aeration capacity and equipment proposed.
NR 110.21(7)(a)(a) Return sludge rate. The rate of sludge return expressed as a percentage of the average design flow of sewage shall lie within the limits shown in Table 6:
NR 110.21(7)(b)1.1. If motor driven return sludge pumps are used, the maximum return sludge capacity shall be met with the largest pump out of service. A positive head shall be provided on pump suctions. Pumps shall also have at least 7.6 centimeter (3-inch) suction and discharge openings.
NR 110.21(7)(b)2.
2. If air lifts are used for returning sludge from each settling tank hopper, no standby unit will be required provided the design of the air lifts allows rapid and easy cleaning. Air lift pumps shall be designed to provide positive control of the return sludge rate.
NR 110.21(7)(c)
(c) Return sludge piping. Suction piping and discharge piping for returning activated sludge shall be at least 10 centimeters (4 inches) in diameter and must be designed to maintain a velocity of not less than 60 centimeters per second (2 feet per second) at normal return sludge rates. Suitable devices for observing, sampling and controlling return activated sludge flow from each settling tank shall be provided.
NR 110.21(7)(e)
(e) Waste sludge pumps. Variable speed or multiple constant speed waste sludge pumps shall be provided. The maximum sludge pumping rate shall be at least 200% of the anticipated volumetric sludge production rate. Devices for measuring waste activated sludge flow rates shall be provided.
NR 110.21 History
History: Cr.
Register, November, 1974, No. 227, eff. 12-1-74; r. and recr.
Register, February, 1983, No. 326, eff. 3-1-83;
CR 09-123: am. (4) (b), (d) 5., (5) (b) 2., 3., (c) 2., (6) (a) 2., (b) 1. and Table 5 (title)
Register July 2010 No. 655, eff. 8-1-10.
NR 110.22
NR 110.22 Physical-chemical treatment. NR 110.22(1)(1)
Applicability. Physical-chemical treatment processes may be used where appropriate to achieve the required effluent limits.
NR 110.22(2)
(2)
Design report. A design report shall be submitted in accordance with s.
NR 110.05 (1). The report shall detail any lab testing, pilot plant studies or operating experience used to design the physical-chemical process.
NR 110.22(3)(a)(a) Chemical selection. Selection of chemicals used in chemical treatment shall be based on the characteristics of the wastewater and constituents to be removed.
NR 110.22(3)(b)1.1. Design of chemical treatment processes shall be based on laboratory testing, pilot plant studies or practical operating experience.
NR 110.22(3)(b)2.
2. Design of chemical treatment equipment, reactors, and appurtenances shall consider:
NR 110.22(3)(b)2.f.
f. The velocity of waste streams in flow conduits to minimize destruction of floc.
NR 110.22(3)(c)1.1. Addition of lime or the salts of aluminum or iron may be used for the chemical precipitation of soluble phosphorus.
NR 110.22(3)(c)2.
2. The addition of polyelectrolytes to aid in the settling of phosphate precipitates should be considered.
NR 110.22(3)(c)3.
3. Chemicals shall be mixed rapidly and thoroughly with the wastewater.
NR 110.22(4)(a)1.1. Eye-wash fountains and safety showers using potable water shall be provided in the laboratory and on each floor level or work location where hazardous chemicals are stored, mixed or slaked, pumped, metered or unloaded. These fountains and showers shall be less than 7.6 meters (25 feet) from points of exposure to hazardous chemicals and shall be fully usable during all weather conditions.
NR 110.22(4)(a)2.
2. Eye-wash fountains shall be supplied with water with a temperature not exceeding 38
°C (100
°F). This supply shall be separate from the hot water supply and be able to provide 15 to 30 minutes of continuous irrigation of the eyes.
NR 110.22(4)(a)3.
3. Safety showers shall be capable of discharging 1.9 to 3.2 liters per second (30 to 50 gallons per minute) of water with a temperature not exceeding 38
°C (100
°F) temperature, and at pressures of 1.41 to 3.52 kilograms force per square centimeter (20 to 50 pounds per square inch).
NR 110.22(4)(a)4.
4. The following protective clothing and equipment shall be available for use with all operations or procedures in which their use will minimize the risk of injury to personnel:
NR 110.22(4)(a)4.a.
a. Chemical worker's goggles or other suitable goggles (safety glasses are insufficient);
NR 110.22(4)(b)1.1. The materials used for storing of hazardous chemicals shall be selected based on the physical and chemical characteristics of each chemical used.
NR 110.22(4)(b)2.
2. Chemical storage areas shall be enclosed by dikes or curbs which will contain the stored volume in case of a spill until it can be either safely transferred to another storage area or released to the wastewater at a controlled rate which will not damage the treatment facilities, inhibit the treatment processes, or contribute to stream pollution. Liquid polymer shall be similarly contained.
NR 110.22(4)(b)3.
3. Chemical storage and mixing areas shall be separate from other treatment plant functions.
NR 110.22(4)(c)1.1. The materials used for piping, valves, pumping, metering, splash guards and any other equipment used to convey hazardous chemicals shall be selected based on the physical and chemical characteristics of each chemical used.
NR 110.22(4)(c)2.
2. All piping containing or transporting hazardous chemicals shall be identified with labels every 3 meters (10 feet) and with at least 2 labels in each room, closet or pipe chase. Color coding may also be used but is not an adequate substitute for labeling.
NR 110.22(4)(c)3.
3. All pumps or feeders for hazardous or corrosive chemicals shall have splash guards which will effectively prevent spray of chemicals into space occupied by workers. The splash guards are in addition to guards to prevent injury from moving or rotating machinery parts. All connections except those adjacent to storage or feeder areas shall have guards which will direct any leakage away from space occupied by workers.
NR 110.22(4)(c)4.
4. Exposed pipes containing hazardous chemicals may not be located above shoulder level except where continuous drip collection trays and coupling guards will eliminate the spraying or dripping of these chemicals onto workers.
NR 110.22(5)(a)(a) Design. Physical treatment shall be evaluated on a case-by-case basis. The design shall be based on pilot plant studies or operating experience.
NR 110.22(5)(b)1.1. Selection of type, size, and depth of filter media shall depend on the filtration rate, the type of treatment provided prior to filtration, filter configuration, available hydraulic head, and the desired effluent quality.
NR 110.22(5)(b)3.
3. For high rate effluent filtration, the filtration rate at maximum hour design flow may not exceed 3.4 liters per second per square meter (5 gallons per minute per square foot). The filtration rate shall be calculated on the total available filter area with one filter unit out of service.
NR 110.22(5)(b)4.
4. Provisions shall be made for backwashing each filter. The backwash system shall be capable of providing a variable backwash rate with a maximum rate sufficient to fluidize the filtering material. A minimum backwash period of 10 minutes shall be provided.
NR 110.22(5)(b)7.
7. Backwash reservoirs shall be provided. Total backwash water storage provided shall equal or exceed the volume required for 2 complete backwash cycles.
